Nanofood Process Technology: Insights on How Sustainability Informs Process Design

Nanostructured products are an actively growing area for food research, but there is little information on the sustainability of processes used to make these products. In this Review, we advocate for selection of sustainable process technologies during initial stages of laboratory-scale developments of nanofoods. We show that selection is assisted by predictive sustainability assessment(s) based on conventional technologies, including exploratory ex ante and “anticipatory” life-cycle assessment. We demonstrate that sustainability assessments for conventional food process technologies can be leveraged to design nanofood process concepts and technologies. We critically review emerging nanostructured food products including encapsulated bioactive molecules and processes used to structure these foods at laboratory, pilot, and industrial scales. We apply a rational method via learning lessons from sustainability of unit operations in conventional food processing and critically apportioned lessons between emerging and conventional approaches. We conclude that this method provides a quantitative means to incorporate sustainability during process design for nanostructured foods. Findings will be of interest and benefit to a range of food researchers, engineers, and manufacturers of process equipment.


INTRODUCTION
Food processing is evolving in its transformation of agricultural raw materials, preservation of fresh and perishable foods, and development of global trade. With the emergence of new technologies, an increasing variety of foods is being manufactured including instant soups and extruded cereals and foods with increased shelf stability and health benefit(s). Importantly, food processing is a matter of "social discussion", with "ultra-processed foods" correlating with the prevalence of obesity 1 and an increasing awareness of the need for sustainability.
The production of nanofoods uses operations common to nanotechnology in other industries, as well as operations from the food industry including the selection of raw materials, design of product(s) for new markets, structural analyses, and promotion of safety. 2−5 Such emerging technologies, however, face the challenge of the need to replace or supplement wellknown and well-defined conventional technologies. A driver for their acceptance is the design new food process technologies with enhanced sustainability.
Sustainability in this context is defined as "process methods and techniques, together with policies that support safety, economic and environmental objectives without placing future potential resources at risk to meet and customize individual human requirements in a way circular and environmentally friendly".
It is hypothesized that knowledge and understanding, i.e., learning lessons, can be drawn from the findings of a significant number of existing sustainability studies of conventional food technologies. This learning is done not by direct transfer of knowledge but rather via joint unit operations, 6 meaning the breaking down of the sustainability lessons to a particular level. This can be done in combination with predictive sustainability tools used in exploratory ex ante, "anticipatory" life cycle assessment(s). 7 Food processing uses unit operations to provide sequential specific changes to raw materials to achieve desired internal properties and deliver palatable and highly nutritional foods demanded in part via consumers and market trends. Understanding this requires knowledge of mass, energy, and momentum transfer, together with the material properties of process intermediates. Food operations can be synergistically combined in a methodology called "hurdle" technology. The name stems from the accumulation of effects to set a hurdle to prevent negative effects on food, e.g., prevent deterioration from bacteria and increase food preservation.
A major goal of nanofood process technology is the dispersion of phases into each other to produce a structured, multi-phase system. Food materials, dispersions, and food processing media have three (3) major physical states, namely, gas, liquid, and solid. An additional fourth state of matter, plasma, 8 has also only recently been reported in food processing as a medium. 9 Another goal of nanofood process technology is to provide the targeted delivery of valuable compounds in a manner similar to what the pharmaceutical industry does with medicine(s). Various unprocessed foods contain nutraceuticals, i.e., bioactive compounds, that provide beneficial components or that positively impact overall wellbeing. 10 Clinical studies have shown a correlation between a daily intake of such nutraceuticals and increased health. 11 Examples include polyunsaturated lipids, vitamins, phytosterols, curcuminoids, carotenoids, and flavonoids. 9 However, nutraceuticals are typically found at low concentration in foods derived from plants and animals. 12 Delivery may also be compromised by chemical instability, low solubility in water, low bioavailability, and/or tightly bound compounds in a food matrix. 11b,13 Nutraceuticals can also be altered by poorly controlled food processes and also during digestion. 14 The food industry and nutritionists have developed "functional foods", 10 aiming to increase the concentration of nutraceuticals in foods or to add nutraceuticals to foods, i.e., to fortify foods. 15 The processing and handling of nutraceuticals are not simple, however, as adding nutraceuticals directly to a food does not predicate desired results. 13 Encapsulation of nutraceuticals prior to incorporation in a fortified food can give physical and chemical stability and control release at the desired site of action. 11b A current drawback of these processing methods for dispersion of phases and delivery of nutraceuticals is that there is little information on the sustainability of nanofood process technology.
In this Review, we (1) appraise the use of food materials, lipids, and biopolymers for forming specific nanostructures including emulsions, liposomes, encapsulates and hydrogels, and nano-architectures and (2) critically assess the transfer of concepts to industrial nanofood technology. For selected nanofood process cases, we (3) determine and quantify the sustainability of joint unit operations with conventional technology and (4) advocate for the selection of sustainable process technologies during initial laboratory-scale developments. We (5) show that selection is assisted by predictive sustainability assessment(s) based on conventional technologies, including exploratory ex ante and "anticipatory" life-cycle assessment, and (6) demonstrate that sustainability assessments for conventional food process technologies can be leveraged to design nanofood process concepts and technologies. We (7) critically review nanostructured foods at laboratory, pilot, and industrial scales, (8) apply a practical method via learning from the sustainability of conventional unit operations, and (9) apportion lessons between emerging and conventional approaches. We (10) conclude that this approach provides a means to incorporate sustainability during design for nanostructured foods and that the difficulty to developing a more generalized and quantitative methodology is that sustainability is unit operation-and food product-specific.
Findings will be of practical interest to a range of food researchers, engineers, and manufacturers of process equipment.

NANO-ARCHITECTURES FOR FOOD PREPARATION
Nanofoods are developed from a wide range of ingredients including lipids, polysaccharides, and proteins. These are used to form a range of materials with varying properties including emulsions, liposomes, and particles.
The range of ingredients, materials, and properties highlight the conceptual diversity of formed nanostructures spanning from nanoemulsions to nanoliposomes. Most findings of nanofoods to date are broadly descriptive. These are explored for a range of food nanostructures below.
2.1. Nanoemulsions and Nanoliposomes from Lipids. Lipid-based nanostructures were developed in the 1990s to address the limitations of lipid-based macrostructures including liposomes and emulsions. 16 Lipid is a collective term for a group of natural molecules that are either insoluble or difficult to solubilize in water, including mono-, di-, and triglycerides, fats, waxes, sterols, and phospholipids. 12,17 Using a lipid as a carrier material for a nanostructure has a number of advantages, including the natural occurrence of lipids in some foods, the essential requirements for lipids in the human diet, and the potential of lipids to provide stored energy. 12,17,18 Lipids are acknowledged as safe as a food additive 12 while potentially providing additional nutritional value as a natural ingredient. 18 Because of their hydrophobic nature, they dissolve lipophilic bioactive compounds readily 18 and lipid-based nanostructures can also encapsulate hydrophilic molecules. Fortified lipid-based nanostructures need to be stabilized with food-grade surfactants, in which selection depends on the nanostructure, lipid, and food. Ionic surfactants and biopolymers are generally not suited to food-grade applications because of the toxicity of surfactants and the tendency to induce gelation of biopolymers. 12,19 Food-grade options therefore include the use of non-ionic synthetic surfactants, with known exceptions, e.g., few natural proteins, such as latherin, are also suited. 12 2.1.1. Nanoemulsions and Microemulsions. The structure of nanoemulsions consists of two (2) immiscible (polar/nonpolar) phases, with one dispersed in the other in which resulting droplets are stabilized via an emulsifier that is similar to a conventional emulsion. Made of oil and water, these structures form either oil-in-water (O/W) nanoemulsions common in food applications or water-in-oil (W/O) nanoemulsions that are more valuable in cosmetic application(s). In OW, oil is the dispersed phase and water is the continuous phase, while in WO, water is the dispersed phase and oil is the continuous phase ( Figure 1). These structures allow bioactive molecules to be carried in the lipid, or aqueous, phase. Compared with conventional emulsions, the characteristic diameter of droplets in a nanoemulsion is typically 20 to 200 nm. 10,11 Because of the "small" size of the droplets, there is no (or not apparent) scattering of light, giving nanoemulsions a near transparent appearance. 19a,20,21 Nanoemulsions are therefore useful for optically clear food products including fortified soft drinks and bottled water. 21 Nanoemulsions, as all emulsions, are not fully stable, meaning in thermodynamic equilibrium, because of coalescence and Ostwald ripening. Droplets get larger with time, adjusting the chemical potential of the droplets to maximize Gibbs free energy. The smaller the droplets, the more significant it is to this effect, and consequently, Ostwald ripening has to be reduced as much as possible to increase the long-term shelf stability of a nanoemulsion. 22 Nanoemulsions have several practically useful functional properties. They are reported to boost the bioavailability of lipophilic bioactive compounds, i.e., the absorption in the gastrointestinal tract and uptake by cells, allowing controlled release at the intended site of action. 21,23 Nanoemulsions are reported to control the release of flavor and coloring compounds that are susceptible to oxidative and photolytic degradation because of aldehyde, ketone, and ester groups. 24 For example, food coatings based on nanoemulsions are reported to improve visual appearance and aroma perception, together with extending shelf-life by incorporating antioxidants, enzymes, antimicrobials, and antibrowning agents. 24 Microemulsions contain droplets of a similar size of 2 to 100 nm. 21 The name can be confusing, because the droplets are not in the micrometer range and are less than those for nanoemulsions. Microemulsions are different to nanoemulsions, because while these consist of the same compounds, oil phase, aqueous phase, surfactant, and often co-surfactant, 11b,25 microemulsions are thermodynamically stable, i.e., the phases do not separate over time, and assembly is kinetically driven. 11b The droplets in a microemulsion can be spherical and nonspherical, and lipids encapsulated either as a core or between tails of surfactants ( Figure 2). 25 However, the state of the microemulsion, i.e., the Windsor Types, is highly dependent on environmental conditions and concentration ratio(s); the system therefore can undergo unwanted changes because of changing temperature or dilution. 11b,21 Microemulsions need comparatively high concentrations of synthetic surfactant; 24 this therefore limits application(s) in the food industry. 19a 2.1.2. Nanoliposomes. Nanoliposomes are spherical vesicles made from an aqueous core and enclosed by one or more lipid bilayers 26 constructed from a lipid-based surfactant, such as a phospholipid that assembles when mixed with water under conditions of low shear stress. 26b This structure allows both hydrophilic and lipophilic compounds to be encapsulated, 27 respectively, within the aqueous core or hydrophobic phospholipid tail ( Figure 3). Select nanoliposome structures are reported to be biocompatible and biodegradable. 27 Nanoliposomes are widely reported for pharmaceutical application. These are practically promising structures for use in foods, although a reported susceptibility to shear means some limitations. They offer practical promise, however, for the delivery of biomolecules, 28 including dermal applications, because of the apparent ease with which nanoliposomes penetrate skin 26a,29 and the range of stimuli that can be used to trigger delivery, 30 including pH, enzymes, glucose, hyperthermia, ultrasound and light, or application of a magnetic field. 27b Nanoliposomes potentially encapsulate both hydrophilic and lipophilic nutraceutical ingredients, flavoring agents, enzymes, and microorganisms. 27a For widespread application, however, the stability of these under conditions of shear and environmental stress needs to be increased, because these can lead to the leakage of bioactive loads. 26 2.1.3. Solid-Lipid Nanoparticles. Solid-lipid nanoparticles (SLNs) are spherical particles in which the lipid carrier is solid at ambient and body temperatures. 18,26b,31 In this way, the lipid carrier retains a crystalline structure following ingestion. 18 The crystalline structure is important to encapsulation of bioactive molecules, namely, these are initially embedded in the lipid carrier in the form of a fortified nanoemulsion that is formed at temperatures above the melting point. 11b, 12 The nanoemulsion is then cooled, leading to crystallization of the lipid carrier with bioactive molecules entrapped within the defects of the crystal lattice. 11b, 12 The diffusion rate for the bioactive molecules is significantly decreased compared with a liquid lipid carrier, protecting the bioactive molecules from untimely release, together with prolonged release at the intended site of action ( Figure 4). 19a The choice and composition of the lipid carrier and resulting crystallization behavior influence loading capacity and "release behavior", together with determining SLN parameters including emulsification temperature and cooling rate. 11b In general, lipids that exhibit polymorphism are preferred, e.g., triacylglycerides (TAGs), because these allow for a greater number of lattice defects, allowing a greater number of bioactive molecules to be included within the nanostructure. 11b, 18 A major disadvantage with SLNs is a decreased loading capacity compared with other nanostructured systems, because the crystalline structure limits the number of bioactive molecules that are incorporated. 11b,19a,26b Importantly, the polymorphic nature of the lipid carrier can be a practical difficulty because polymorphic transitions during storage can lead to drug expulsion, called "burst release", 19a,32 or induce gelation. 33 2.1.4. Nanostructured Lipid Carriers. Nanostructured lipid carriers (NLCs) were developed to overcome limitations of SLNs, and they are described as modified SLNs. 26b The carrier matrix is not (exclusively) made of crystalline lipids but also consists of a mixture of lipids with melting points above and under a healthy body temperature (36.8°C), leading to particles that contain both solid and liquid structures at room and body temperatures. 18 To obtain an NLC lipid carrier matrix polymorph, solid lipids are mixed with unsaturated fatty acids at temperatures above the melting point. 18 When the precursor nanoemulsion is cooled to induce solidification of the polymorph lipids, solidification is modified by the liquid components of the matrix. For example, for imperfect NLC with crystalline and liquid sections in the lipid core, 19a,26b the unsaturated fatty acids inhibit formation of highly ordered crystal lattices and increase the number of lattice defects compared with SLNs, increasing loading efficiency, which is the ratio of actual to theoretical bioactive nanomaterial content. 18 Concurrently, many hydrophobic bioactives exhibit increased solubility in a liquid lipid compared to a solid lipid, 10 easing incorporation of bioactives. However, the solid structures in NLC prevent diffusion of bioactives into the aqueous phase, i.e., prevent degradation from environmental influences, and allow a controlled release of bioactive at the intended site of action. 19a Selection and composition of the NLC lipid carrier matrix, together with the bioactive, significantly influence structural characteristics of the resulting nanostructure, e.g., crystalline packing and rigidness, and NLC production parameters. 18,19 The liquid lipids are reported to "slow down" polymorphic transitions of the solid liquids, thereby improving stability. 19a,26b In particular cases, crystallization is inhibited, leading to an amorphous solid structure of solid lipid. 19a NLC is therefore a complex system, and components need to be selected carefully. Additionally, lipids like cholesterol or saturated lipids can be used as solid lipid in NLC, but this is undesirable, given the potential risk to health ( Figure 5). 19a 2.2. Nanohydrogels, Nanoencapsulates, and Nanoemulsions from Biopolymers. The term "biopolymers" describes polymers that are obtained from a natural source, e.g., animals or plants, and mostly refers to protein and  polysaccharides. Biopolymers are preferred to synthetic polymers, many of which are not of food grade, because of association with inflammatory reactions and toxicity and are also costly to produce. 14a Most biopolymers that are obtained as by-product(s) or waste(s) in agriculture and the food industry are non-toxic. The use of biopolymers as a nanostructure matrix is different when using lipid-based nanostructures. While physicochemical characteristics of lipid-based nanostructures result from intermolecular interactions of its components, biopolymers are selected based on physicochemical properties of the polymer chains that are adjustable via intramolecular change(s). Therefore, biopolymer nanostructures and bioactive binding sites can be designed on a molecular level for selected application. While biopolymers exhibit practical promising characteristics for the design of nanostructures for the food industry, they are not often used. 11b,19a Practical difficulties include the low availability of biopolymers with consistent quality, required use of organic solvents during production, and the absence of large-scale production. 11b,34 However, for functional properties, biopolymers are considered valuable as food additives and used as emulsifiers to stabilize lipid-based micro-and nanostructures. For example, Gum Arabic, a gum obtained from certain Acacia trees, is commonly used as an emulsifier in beverages. 34 2.2.1. Protein-Based Nanostructures. Proteins are biopolymers, with monomers of one or several amino acids. Animal and plant sources are commonly used in the food industry. 35 Production can readily be incorporated into existing processes, giving opportunity to valorize former waste streams, e.g., producing gelatin from collagen found in the skin and bones of animals. 36 Therefore, proteins are generally considered as inexpensive and label-friendly functional ingredients in processed foods while providing nutrition and being biodegradable, biocompatible, and non-toxic (GRAS, "Generally Recognized as Safe" by Food and Drug Administration). 14a, 35 Practical functionality includes emulsifying, jellifying, and foaming properties, 14a,37 therefore significantly impacting sensory properties of final food product(s). 35 These functional properties stem from molecular characteristics, i.e., the arrangement, number, and type of amino acid residues, the electrical charges in the biopolymer chain, and tertiary and quaternary structures that impact intra-and intermolecular bonding to influence hydrophobicity, aggregation, and network formation by the protein structure. Intermolecular bonding is also influenced by environmental conditions including temperature, pH, and ionic strength. 14a, 38 Specific protein nanostructures incorporated in a food can include hydrogels, solid particles, or emulsions. 35 Nanohydrogels are especially of interest, as they can be formed readily from proteins without incorporating synthetic polymers. Hydrogels can also consist of polysaccharides or of a mixture of proteins and polysaccharides ( Figure 6). 39

Polysaccharide-Based Nanostructures.
Polysaccharides are a group of hydrophilic polymers in which monomers are monosaccharides connected via a glycosidic bond 13,40 ( Figure 7). Because of a natural origin from animals, plants, algae, and microorganisms, 41 they share advantages with proteins including biocompatibility, biodegradability, renewability, availability, and (relatively) low toxicity. 13,41b,42 In contrast with proteins, polysaccharides exhibit low immunogenicity. 41b As food additives, polysaccharides provide a range of functionalities including improving the thermostability of foods and modification of texture and structural properties. 43 Polysaccharides are available in a myriad of forms, including hydrolyzed and functionalized forms, and are therefore widely used in the food industry. They are mainly sourced directly from agricultural ingredients. When sourced within the food  industry from by-product streams, complex purification is sometimes needed because of complex polysaccharide structure(s) and other by-products and impurities. 41b Polysaccharide-based nanostructures for encapsulation have been more generally researched for controlled release of drugs in medical application(s). Consequently, many of the nanostructures intended for food fortification have originated from medical research and have been applied in the food industry. Because major groups of polysaccharides are not soluble in acids, polysaccharide-based nanostructures withstand the hazardous environment of the stomach and transport bioactive molecules to the colon, an important site in the gastrointestinal tract for absorption of bioactives. Among polysaccharide/biopolymer-based nanostructures are nanocapsules that are spherical vesicles with a polar, or a nonpolar, core and a polymeric shell. For medical application, chitosan and alginate are used as shell materials. Biopolymer nanocapsules can also be obtained from proteins including zein and casein. 39 Additionally, polysaccharides have been reported as potential functional additives in a range of inorganic nanostructures with matrix materials including, Au, Ag, C, and graphene, resulting in "polysaccharide-based nanocomposites". 41b To better understand the selection of structures described in this section, Table 1 includes a summary of literature references of specific examples where each architecture is used, the construction materials, and the embedded nanomolecules applied to food processing.

Sustainability Lessons from Conventional Food Technologies.
The reported nanofood process technologies reviewed above lack adequate or sufficient information on potential process sustainability, as well as lacking life cycle assessments of the process steps used to structure and produce nanofoods. However, in this absence of understanding, useful comparisons are available from established sustainability studies of conventional food technologies that can be used for learning in nanofood technologies.
Both nanofood and conventional food processes share general dependencies on raw materials and regional resource supply and also share unit operations from chemical, mechanical, and electrical engineering. Usually, one of these operations determines process sustainability. Lessons can therefore be drawn between food processes at the level of this unit operation despite the potential differences in the details of technologies. An efficient heating concept, for example, will likely add efficiency when applied across different systems. Table 2 presents the common engineering operations connected with nanofood processing technologies. It also includes a summary of the sustainability lessons that can be drawn from judicious consideration of shared engineering operations in nanofood technologies and conventional food processing. Sustainable aspects include energy, water, global warming potential, and terrestrial acidification, that is, quantification of changes in soil chemical properties caused by atmospheric emission of pollutants affected by processing; Figure 7. Examples of nanocapsules with a lipid or an aqueous core encapsulating hydrophobic bioactive molecules or hydrophilic bioactive molecules, among a variety of available techniques and materials. these include nitrogen oxides (NO x ), ammonia (NH 3 ), and sulfur dioxide (SO 2 ). These gases impact ecosystem quality, leading to changes in pH that weakens plant growth and failure of seeds to germinate. 65 Nanofood processing therefore needs to "adopt, adapt, and optimize" sustainable engineering operations. There are a number of lessons from conventional food process technologies that have been understood and have been or could be applied practically to nanofood development. Sustainability lessons are generally available via the impact of a main unit operation.
3.2. Generalized Sustainability Lessons. Important sustainability lessons for the food industry common to both conventional and nanofood processing include (1) greenhouse gas release (GHG), with the food industry responsible for ca. one-third of global emissions, 66 (2) freshwater consumption, with food processing accounting globally for the third highest water consumption and wastewater discharge 67 where in the United States, this represents ca. 80% of the total consumption, 68 (3) energy consumption, ca. 5% of the total industry, 69 and (4) chemical pollution, including that from mineral fertilizers and pesticides. 70 3.2.1. Raw Materials. Raw material production, including crop cultivation and animal husbandry, generates the most significant environmental impact within food production, including land-use change, reduction in biodiversity, freshwater eutrophication (overfertilization), global warming (fermentation gas emissions), water shortages (over irrigation), ecotoxicity, and human toxicity (fertilizers and pesticides). 71 Food process technology contributes ca. 10 to 20% of the total environmental impact from the food industry. 72 This will likely be decreased via process optimization(s) in common, global food unit operations, including drying, heating, and freezing.
3.2.2. Regional Variance. Because ecosystems, nationally and locally, rely on geographical climatic and soil variance and farming practices, there are significantly different sustainability outcomes from Life Cycle Assessments (LCA). 72 While some aspects of food processing are common regardless of geographical region, others vary, including the energy-mix. For example, the LCA impact of food processing using German energy sources of 15% nuclear and 55% fossil was 4 to 5× greater than French energy sources of 76% nuclear and 6% fossil. 73

Benchmarking of Food Unit
Operations. Global warming potential (GWP) is an acknowledged measure for benchmarking the potential impact of essential unit operations in food manufacturing. The GWPs for three (3) common operations, namely, drying, heating, and cooling, are summarized comparatively in Table 3 for a range of selected foods.
It is seen in the table that the value for GWP ranges from ca. 0.42 to 2.67 kg CO 2 -eq kg −1 . This impact is significant and evident when understanding that it is similar in value to the synthesis of NH 4 through the Haber−Bosch process (HBP). (Incidentally, this consumes the greatest energy in the chemical process industry with 1.5 to 3.0 kg CO 2 -eq kg −1 .) The range of values relates both to specific diversification in unit operations, for example, drum, freeze, spray, and infrared forms of drying, together with food type, for example, apples, strawberries, apple pulp, and apricots. A drawback however is that the reported literature does not permit a quantitative separation of both these effects.

Impact of Additional Food Unit
Operations. The data of Table 3, while practically useful, present a simplified view with focus on individual unit operations. For a more complete assessment, the whole process including any additional unit operations needs to be considered.
Because milk processing is widely studied and understood globally, it serves as a practically useful example. The cascade of unit operations used to produce a range of dairy products from milk is presented in Figure 8. A common environmental impact for all products arises from raw material production based on feeding of animals, solid wastes, and gaseous emissions of CH 4 . It can be usefully noted here that upstream operations, including animal or vegetable production, account for one-third of global greenhouse emissions (GWP) 66 and 80% of freshwater consumption in the United States, 68 while mineral fertilizers and pesticides are globally a main source of air and water pollution. 70 In Figure 8, Operation 1 is a thermal treatment for milk preservation. GWP data are seen to be similar for different milk products, confirming that using the same important operation on different ingredients with varying protein, fat, and water content provides comparable sustainability for this operation. Once the milk is pasteurized, different operations can follow for milk-product diversification, unless milk and cream are the end-products. Operation 2 with ripening, inoculation/ incubation, and drying increases GWP impact ca. 4× compared with Operation 1. The "smoking" product in Operation 3 has a significant GWP.  Figure 8. Schematic for accumulated GWP with successive unit operations in processing of milk to dairy products. This analysis demonstrates the effect of additional operations that sum to give the "total" impact in food manufacturing.
Maximal cumulated GWP for cheese is 10× greater than for milk when smoking is included (although this is not common for all cheeses), and yogurt is 2× that for milk, underscoring the significant impact of successive process steps.

PROCESS-SPECIFIC SUSTAINABILITY LESSONS FOR NANOFOOD PROCESSING
Operation-specific lessons for the sustainability of nanofood products are especially important and include electrically, thermally (heating and cooling), and dispersion-driven processes. 4.1. Electrically Driven Nanofood Technologies and Operation-Specific Sustainability. Lessons can be drawn for nanofood structure generation from comparison with conventional processes of electrospinning and electrospraying and from conventional evaporation or drying.
4.1.1. Electrospinning. Electrospinning generates encapsulated solid nanoparticles when a fine powder particulate is dispersed in a spinning dope. Electrospuns are produced via injection of a polymer/biopolymer solution from a spinneret into a prepared collector, 85 as shown in Figure 9. The nanofiber has a large surface-to-volume ratio and is used as a carrier for bioactive food ingredients and nutraceuticals. 86 At the laboratory scale, a syringe pump is used to impulse the spinning liquid through a spinneret fabricated from a hypodermic needle. The needle is charged via electrical connection. 87 Following the spinneret, a collector is placed that is (usually) a stationary metal plate or foil connected to the ground to remove residual surface charges.
Coaxial electrospinning is used to control the release of encapsulated food compounds including nutraceuticals, proteins and enzymes, or bacteria. For example, Bif idobacterium can be encapsulated in poly(vinyl alcohol) and used to produce 150 nm fibers. 88 Two-component fibers are extruded from two (2) polymers using coaxial electrospinning with two spinnerets, one inside the other (Figure 9), 85,89 where the inner core material has greater viscosity. 90 A range of food-grade polymers is used for electrospinning to entrap, coat, or encapsulate proteins (e.g., casein, soy and whey, gelatin, albumin, collagen, zein, and wheat gluten), carbohydrates (e.g., alginate, chitosan, pullulan, guar-gum, tragacanth, inulin, cellulose, and dextrans), lipids (e.g., phospholipids), and animal/vegetal-origin synthetic polymers (e.g., polyvinyl alcohol and poly(ethylene) oxide). Bioactive compounds are then included via simple mixing into polymer spinning solution(s). 91 However, at present, scale-up has a number of limitations. When spinnerets are arranged in arrays, the electrical field gets weaker from the edge to the center. 92 The electrostatic force used to produce fiber from the spinneret reportedly then becomes a rate-limiting step.
An example scale-up however is the Nanospider electrospinning technology developed by Elmarco (www.elmarco. com). The process includes a rotating cylinder charged to 32 to 43 kV half-immersed in spinning dope. 93 The liquid film is broken to form fibers collected above the tubular emitter. 72 Nanolayr reported this scale-up of electrospinning. 94 4.1.2. Electrospraying. Electrospraying, or electro-hydrodynamic atomization, produces nanoparticles using high voltages, converting liquids to fine droplets that are stretched toward a ground electrode where the solvent is vaporized. The formation of nanocapsules is influenced by many parameters, including voltage, liquid velocity, collector distance, viscosity, density, concentration, pressure, and temperature. 95 Conventional electrospraying is shown schematically in Figure 10, where an electric field is used to split droplets into nanometer size by reducing surface tension via electric charge generation in a droplet. 96 Particles are generated below the Taylor cone and collected on an Al plate. Process examples include production of wool keratin 97 and zein films 98 and encapsulation of curcumin in gelatin. 99 A variation for this process involves electrospraying in solution, where charged droplets are collected in a crosslinking solution, typically calcium chloride. Two (2) polymer solutions are released concurrently using two (2) concentric needles of different diameters. This is known as electrospray electro-coextrusion. 100 Active ingredients can be electrosprayed separately or together with a carrier polymer. 101 Food examples include lycopene encapsulated in edible polymer matrices of dextran, chitosan, and whey protein concentrate. 102

Sustainability Lessons from Conventional Evaporation and Drying.
Electrical process technologies involved in nanofood preparation, including electrospinning and electrospraying, comprise (1) ohmic heating, (2) electromagnetic activation, (3) evaporation or drying, and (4) high-pressure processing.  Lessons from conventional food technologies are available therefore from (3) evaporation or drying.
Drying, including evaporation, accounts for most thermal energy and electricity consumption within food processing. For milk powder production for example, this is ca. 44% of the total fuel consumption, equivalent to 616 MJ kg −1 . 82 Across the food industry, drying contributes ca. 25% of the total energy consumption. 103 The environmental impact of drying is greater with longer operational times and/or higher temperatures. 103 As is evident from Table 3, the impact depends on the type of drying and food ingredient(s), with an energy consumption similar to that for HBP.
A reported means to reduce energy consumption is to combine non-conventional drying methods, such as dehumidification, with conventional high-temperature drying. In this way, GWP can be reduced to ca. 48% and terrestrial acidification potential (TAP) can be reduced to ca. 59% for apricots by sequentially using osmotic dehydration and freezedrying. 75 Microwave drying of sardines reportedly reduces energy consumption by 55% 104 and similarly for bananas. 105 Combining infrared with hot air is demonstrated to accelerate drying. 106 Combined microwave−vacuum drying has been reported for sea products, 107 combined microwave−osmotic dehydration for pineapple, 108 and combined microwave− freeze drying for jujube fruits. 109 Other combinations have included combined infrared−freeze drying for mango 110 and combined infrared−microwave drying for cake. 111 Timevariant modulation has been applied to pulse-spouted microwave−vacuum drying, 112 pulse-spouted bed microwave−freeze drying 113 and microwave−freeze drying. 113 To exemplify how the sustainability of conventional operations can be reduced, the energy consumption is taken. Two beneficial effects can be utilized. First, their industrial scale-up would optimize the heating per production unit, both per new design and by compactness (relatively less energy sources), the latter meaning less surface relative to the volume increase. Second, the energy source could be shifted toward renewables replacing the current gas or fossil fuel energy sources, either indirectly by using an electrical grid with high renewable share (could be an at-site microgrid) to change electricity to heat or by directly using renewably made electricity for heating. Both measures would allow a reduction in environmental impacts such as GWP, acidification, and depletion of abiotic resources.

Conventional Drying Technologies.
Conventional drying including air and sun is common because of low cost and simple operation. 9 However, drawbacks include high energy demand, long drying time(s), and the potential for poor product quality from reduced sensory perception and nutritional value. 114,115 The addition of an agent to lower water activity including humectants, e.g., sucrose, trehalose, or glycerol, 116 results in osmotic dehydration by reducing the amount and mobility of water; however, this can induce negative effects on flavor, nutrition, and health. 117−119 Taste alteration(s) and longer processing times have been reported. 120 The interaction of electromagnetic waves with organic matter in electromagnetic drying can be selective to particular molecules rather than just heating the whole food. 9 In this process, which is used to dry beef jerky 121 and pork slices, 122 energy is not always homogeneously distributed, causing "hot spots". Other technologies include microwave and infrared 123 and ultraviolet light, which is reported in some food applications, 124 such as application in legume cakes. 111 Rarely used are electron, X-ray, and gamma irradiation 125,126 because these reportedly can ionize harmful microorganisms and damage valuable food components. 8 Combined modes are reported including electroosmotic dewatering for tomato paste 127 and electroosmotic-pressure dewatering for vegetable sludge. 128 These combined conventional technologies can be useful for lessons in nanofood process development. For example, drying by infrared irradiation, combined with superheated steam, results in a lower GWP of 0.71 kg CO 2eq kg −1 for drying apricots 129 as compared with drum-drying of apple pulp, which releases 2.67 kg CO 2 -eq kg −1 . 74 4.2. Thermally Driven Nanofood Technologies and Operation-Specific Sustainability. Lessons on operationspecific sustainability can be drawn from a comparison with conventional heating of thermally driven nanofood technologies based on nanospray drying for nanofood structure generation.
4.2.1. Nanospray Drying. Nanospray drying uses a laminar drying gas that is projected toward a vibrating-mesh spray to form fine droplets, producing nanoparticles through an electrostatic precipitator. This process is adapted from conventional spray drying (Figure 11, left). Encapsulation is achieved by dissolving, emulsifying, or dispersing the core material in a carrier solution, including gums, carbohydrates, and/or proteins. Because solvent evaporation keeps droplet temperature low, the process can be used with heat-sensitive product(s). 130 Nanoparticles can be made with relatively few process adaptions (Figure 11, right), with nanoparticle size and morphology targeted via process control. Nanospray drying is relatively "simple", with short processing times. Costs are low compared with other drying technologies, such as freeze drying. 131 Nanospray drying involves three (3) steps (Figure 11, left), namely, (1) atomization, (2) drying of nebulized droplets in a hot gas with solvent evaporation and corresponding particle formation, and (3) separation of dried product(s) using a cyclone in a conventional process (left) or particle collection in conventional processing (right). Particle deposition on the chamber wall is reduced via the laminar flow of drying gas, vibrating mesh spraying, and electrostatic particle collectors (Figure 11, right). 132
Lessons from conventional food technologies are available therefore from (2) heating.
Thermal processing using steam and hot water is "standard" in the food industry. However, disadvantages include a necessary high investment in energy 134 and a decrease in the sensory and nutritional value of the food. Environmental impact(s) from thermal processes depend significantly on treatment conditions. For example, the GWP for pasteurized milk ranges from ca. 0.114 to 0.427 kg CO 2 -eq L −1 and that for ultra-high temperature (UHT) processing ranges ca. 0.212 to 0.594 kg CO 2 -eq L −1 , because UHT 77 consumes greater energy. Thermal processing of milk and milk cream increases terrestrial acidification potential (TAP) because of energy consumption, together with subsequent wastewater generation. 135 For orange juice processing, for example, pasteurization, blending, and cooling share ca. 20% of impacts, 136 while for apple juice processing, the share is ca. 33%. 137 For some foods, additional food operations add to the environmental impact, for example, pasteurization, molding, and salting or ripening used to produce cheese. Kim et al. quantified GWP and freshwater eutrophication potential (FEP) for cheddar cheese production to, respectively, 0.59 kg CO 2 -eq kg −1 and 0.43 × 10 −3 kg P-eq kg −1 . 138 Gonzaĺez-García et al. assessed Galician and mature cheese at, respectively, GWPs of 1.92 and 1.39 kg CO 2 -eq kg −1 and FEPs of 8 × 10 −3 and 9.1 × 10 −3 kg P-eq kg −1 . 139 Smoking is used as an additional operation to give food a particular flavor. This needs wood and fuel combustion. GWP accounts for 1.92 kg CO 2 -eq kg −1 for smoked cheese, together with an increase of 20% for GWP and 40% for TAP. 83 4.2.3. Conventional Drying Technology. Heat transfer occurs via convection, conduction, and/or radiation, with water (including steam), air, and oil as common transfer

ACS Sustainable Chemistry & Engineering pubs.acs.org/journal/ascecg
Research Article media. Heating inactivates pathogens, preserves foods, 140 and improves digestibility and nutrient bioavailability. 141 Thermal treatments can be classified as thermization or subpasteurization, with some pathogens developing resistance, 142 pasteurization, e.g., for kiwi jam, 143 fresh pasta, 144 meat, 145 and honey, 146 ultra-high-temperature treatment, which is fast but can impart undesired flavor changes, 147 sterilization, in which destroying all microorganisms, including most spores, 148 can also result in unwanted sensory change(s), 148 and ohmic heating 149 for microorganism and enzyme inactivation, 150 which is accompanied by a reduction in the size of protein aggregates and changes in protein morphology and physicochemistry 151 and immunoreactivity. 151 A combined mode of heating with refrigeration, followed by thermization and a second refrigeration, can potentially be used for cheese and/or protein whey. 152

Cooling-Driven Nanofood Technologies and Operation-Specific Sustainability. 4.3.1. Desolvation of
Protein-Based Nanoparticles. Lessons can be drawn for the desolvation of protein-based nanoparticles and nanocrystallization from the conventional processes of cooling, including cooling using mechanical and fluidic treatments. A desolvating agent can be used to precipitate biopolymers, e.g., proteins. Gelatin, albumin, collagen, milk proteins, silk protein, elastin, zein, gliadin, and soy protein have all been used. 153 For example, Ipsen and Olsen described the conversion of αlactalbumin to nanotubes. 154 These gels are mechanically resistant, reversible, and pH-sensitive and are able to encapsulate vitamins and/or enzymes. 155 A range of other morphologies are also possible.
4.3.2. Nanocrystallization. Nanocrystallization refers to precipitation (bottom-up) or size reduction of larger crystals (top-down) as a means to define nanocrystal size 156−158 and can involve a range of techniques, some of which involve cooling ( Figure 12).
Commonly, top-down processing involves wet milling, including (1) bead milling (Nanosystems-Alkermes 159 ), combined with (2) high-pressure homogenization and smartCrystal technology (fast and smaller size production of nanocrystals than first-generation top-down or bottom-up methods). In bead milling, a macro-suspension is produced when a powder is dispersed in a stabilizer solution that is recirculated several times through the bead-mill chamber ( Figure 13). A coolant also reduces the temperature during milling. Particle size reduction is a result of shear forces produced by moving beads and the collision of particles. Disadvantages include the production of low nanometer particles and the need to remove all solvent traces.
High-pressure homogenization reduces particle size by shear force(s), particle collisions, and cavitation. Two (2) variants are reported. 161 Microfluidization collides two (2) crystal suspensions under a pressure of 1700 bar. Piston-gap homogenization forces through a small nozzle, creating a sudden pressure gradient. Disadvantages are the need for micronized starting material and long runtimes. 157 Combined technologies reportedly have practical promise to overcome these limitations. NANOEDGE technology, 162 H42 technology, 163 and H96 technology 164 integrate microprecipitation, spray drying, and pearl milling. H69 methodology leverages smartCrystal technology with cavitation taking place concurrently with particle formation. This is called caviprecipitation. Collision and shear forces stop nucleation and prevent further crystal growth. Examples include the microfluidizer and EmulsiFlex C5 from Avestin. 165 4.3.3. Sustainability Learning from Cooling. Cooling nanofood process technologies involve (1) heating, (2) cooling, (3) mechanical treatment, (4) electromagnetic activation, and (5) evaporation.
Lessons from conventional food technologies are available from (2) cooling and (4) electromagnetic activation.
Food process freezing at temperatures of <−18°C is used to secure high-quality frozen goods that maintain original flavor, color, and nutrition. These are commonly preceded by prefreezing. Depending on the nature of raw materials, prefreezing is accompanied by other secondary operations, including washing, peeling and cutting, sorting, or blanching. 166 Freezing exhibits lower LCA as compared with raw food production. 166 Freezing has an environmental impact of similar GWP to drying and heating. Ilari et al. reported for freezing green beans a GWP of 0.7 kg of CO 2 -eq kg −1 , abiotic depletion potential of 9.5 MJ-eq kg −1 , fresh water ecotoxicity of 0.2 kg 1,4-DB-eq kg −1 , and marine aquatic ecotoxicity of 312 kg 1,4-DB-eq kg −1 . 166 For broccoli, the overall environmental impact increased by 25 to 50% when compared with fresh food, with the exception of the eutrophication potential, which decreased. 84 Abiotic depletion potential for frozen broccoli was 1.71 × 10 −2 kg Sb-eq kg −1 , acidification potential was 9.32 × 10 −3 kg SO 2 -eq kg −1 , eutrophication potential was 4.49 × 10 −3 kg PO 4 -eq kg −1 , GWP was 2.64 kg CO 2 -eq kg −1 , and photochemical oxidation potential was 7.71 × 10 −4 kg C 2 H 4 -eq kg −1 . 84

Sustainability Lessons from Electromagnetic
Activation. Non-thermal processing, including high pressure (HP), ionizing irradiation, and pulsed electric field (PEF), provides alternatives to thermal treatment, together with a claimed reduction in the negative impact on food quality with increased energy efficiency. 167 However, there is inconsistent reporting of efficiency as exemplified by Davis et al. 168 who report an HP of 0.23 MJ L −1 and PEF of 0.17 MJ L −1 to be more energy-efficient than thermal treatment of 0.26 MJ L −1 for carrot juice, whereas Aganovic et al. report 3 to 5× greater energy demand for nonthermal processing with 0.72 MJ L −1 HP and 0.43 MJ L −1 PEF compared with thermal treatment of 0.14 MJ L −1 for tomato and watermelon juice. 134 It is concluded therefore that caution must be exercised with generalized statements for classes of food technology; rather, performance will necessarily be a function of the food and technology used within a given class.
For GWP, however, the trend is clearer. The GWP (CO 2 -eq kg −1 kg) ratios for thermal treatment to HP for tomato salsa, 167 ready-to-eat meal, 169 and milk 170 are reportedly, respectively, infinite, 2.7, and 8.7. Valsasina et al. confirmed that HP has 83% lower carbon footprint for milk homogenization, as compared with thermal treatment. 170 Mikhaylin et al. report applying bipolar membrane electrodialysis with ultrafiltration with 10% lower environmental impact, as compared with conventional acid−base processing that uses hazardous chemicals. 171 172 However, cooling can cause undesired structural damage(s), including crystallization and cell destruction, with the release of intracellular contents. 173 Freezing can be combined with osmotic drying, 174 as reported for mango 175 and tomatoes. 176 Mechanical treatment uses applied force for reversible, e.g., sorting, or irreversible, e.g., milling, material deformation. 177 High static or dynamic pressure(s) changes the distribution of compounds in foods and renders microbes non-viable 178,179 and lowers the energy demand for added value, e.g., in artificial meat production. 180 Osmotic pressure allows removal of water from food, together with introduction of solutes, 181 e.g., kiwi slices. 182 Vacuum impregnation brings fluids into food and removes deleterious reactive gases, including oxygen. 183 Drying rates are faster than by drying alone, canning, freezing, or frying pretreatment. Combined with osmotic dehydration, 183 gases are removed from capillary pores, 184 and the osmotic solution flows into the pores. 185−187 For Spanish cured ham, process times 188 were significantly reduced, and calcium-fortified pineapple snacks resulted in an improved sensory profile with long storage. 189 Drawbacks however included poor mass transfer control and practical obstacles to the reuse of hypertonic solution(s). 190 Ultrasound technology is reportedly used for fluid transport in meat tenderization, either continuously or pulsed-applied 191 via pressure, temperature, or volumetric compression/ expansion changes(s). 191 Combined with osmotic dehydration, ultrasound creates microscopic channels in tissues to ease gas− osmotic solution exchange, 192 e.g., in potato 193 and Malay apple. 194 4.4. Dispersion-Driven Nanofood Technologies and Operation-Specific Sustainability. Lessons can be drawn for nanoemulsions and nanoliposome formation from the conventional processes of extraction and postprocessing operations.

Nanoemulsions. Tadros et al. classified nanoemulsion
techniques according to energy demand into high-energy and low-energy ones. 195 Nanoemulsions need to be made with control over droplet size and size distribution. 196 The choice of technique depends on ingredients and properties such as stability. Nanoemulsification uses high-pressure homogenizers with 99.8% of energy spent to produce heat. Therefore, chemical degradation of food materials can occur. 197 Additionally, entrapment of air needs to be avoided to prevent unwanted foam formation. 198 Operational integration is as important as for other food process technologies. Nanoemulsification is usually carried out in multiple steps, starting from separate oil and water solutions that are transferred in a high-speed colloid mill at revolutions of up to 30,000 rpm with controlled accelerations and decelerations to produce high tangential forces. Different internal shear regions are utilized. This avoids coalescence. 199 Microfluidizers and ultrasonic homogenizers are used for prehomogenization, while high-pressure homogenizers deliver pre-emulsions. 200 In addition to energy demand(s), homogenization is carried out in either a hot or cold environment (Figure 14). This is governed by the melting point of the hydrophobic phase, viscosity to prevent degradation of functional materials and heterogeneous distribution of the phases, and complex crystallization during cooling. 32a Following pre-homogenization, a second homogenization step is used to reduce droplet diameter to a nano-size range. High-pressure valve homogenizers with a gap of 10 to 100 μm are used at pressures in the range of 100 to 500 MPa together with refrigeration for cooling ( Figure 15). 202 An example is that microfluidizers pre-homogenize emulsions under pressures of 35 to 140 MPa and then pump the fluid to a microchannel section, generating a flow of high turbulence. 130 At the outlet, the fluid is ejected as elongational flow for adsorption of the emulsifier to form interfaces. 203 High-pressure valve homogenization is used to generate essential oils and to encapsulate bioactive ingredients. 204 Ultrasound is also reportedly used to reduce droplet diameter. High-intensity ultrasonication produces up to 100 nm nanodroplets operating at a frequency of 16 to 100 kHz and a power density of 10 to 1000 W cm −2 . As stability is improved, less emulsifying agent is needed compared to preparations made with high-pressure homogenizers. 206 Sizing sonochemical reactors to the industrial scale is a practical challenge because of physical limitations of the technology. This technology has the potential, however, for reduced production costs and equipment contamination compared with microfluidizers. 207 Pascual-Pineda et al. reportedly prepared a paprika oleoresin nanoemulsion 208 using these techniques.
In opposition to high-energy methods, low-energy methodologies are based on phase inversion by changing the hydrophilic−lipophilic balance via either temperature or composition. 200 However, this technology requires a greater concentration of surfactants and greater dispersity of droplets. Phase inversion is achieved by adding water to a stirred oil− surfactant mixture to change the O/W ratio toward an excess of water, reversing dispersity to give an oil-in-water suspension. 197 Alternatively, heating to above the temperature for phase inversion changes the solubility of the surfactant, inducing a phase transition that changes the emulsion type. 209 Rapid cooling then freezes this phase change. 210 In membrane emulsification, the dispersed phase is pressed through a membrane that forms emulsions directly, or this technique can be used to premix. 211 Major process parameters include membrane type, pore size, cross-flow speed, pressure, and type of emulsifier.
4.4.2. Nanoliposomes. Conventional methodologies for producing nanoliposomes include (1) thin-film hydration, (2) solvent injection, (3) detergent removal, and (4) reverse phase. Methodology (1) is based on aqueous rehydration of thin phospholipid films initially dissolved in an organic solvent. Once the solvent is evaporated, the film is composed of the encapsulates. The concept for methodology (2) involves the solubilization of the hydrophobic fraction in an aqueous system using a solvent, e.g., ethanol. In methodology (3), an excess of surfactants is eliminated once micelles are produced using dialysis. In methodology (4), the dissolution of lipids in a solvent to form a water-in-oil emulsion is utilized. Liposome formation is preceded by solvent removal in the aqueous dispersion.
These four (4) methodologies have drawbacks including (1) the large size of liposomes, (2) remainder of solvent traces, (3) destabilization induced by temperature changes, and (4) low reproducibility. 212 Supercritical fluid technology, dual asymmetric centrifugation, membrane contactor technology, cross-flow filtration technology, and freeze-drying technology have practical promise to obviate these drawbacks. The goal is to minimize destabilization, as well as degradation. This can be achieved by controlling the composition, temperature and pH, nature of the materials, ionic strength, and sensitivity to light or oxygen. 213 In an alternative method, the dissolution of lipids, e.g., phospholipids and cholesterol, in supercritical CO 2 (scCO 2 ) allows for a supersaturation state that facilitates precipitation to ultrafine particles following the release of CO 2 . Liposomes are obtained by concurrently adding an aqueous phase. 214 A variant is supercritical reverse phase evaporation for liposome production using scCO 2 as a solvent for lipids ( Figure 16). 215 Dual asymmetric centrifugation has double-axis rotation, one centering vials and the other a centrifuge. Material is pushed in an outward direction, while concurrently, material is pushed in the opposite direction because of adhesion, which reportedly works well with viscous material(s). 216 This methodology allows the compactness of equipment, good reproducibility, the formation of small liposomes without the need of additional operations, and high entrapment efficiency. A minimum phospholipid concentration is required for sufficient viscosity. 212 Membrane contactors disperse lipid and water phases to form liposomes. While the aqueous phase is pumped through the membrane contactor, the lipid phase is pumped perpendicularly, permeating the internal pores of membrane fibers of the contactor. Liposomes are formed "spontaneously" once both phases meet. Advantages include ready scalability, reproducibility, small size dispersion, and high encapsulation efficiency. 217 Cross-flow filtration technology pumps the mixed micelle solution through a pressurized membrane. The pressure acts to  remove the surfactant. Advantages are fast production and filtrate recycling to minimize waste. 218 Freeze drying uses cryoprotectants, such as carbohydrates, to facilitate transition of liposome suspension to liposomes, with sizes <200 nm. 219,220 4.4.3. Sustainability Lessons from Post-Processing (Including Extraction). Dispersion-driven nanofood process technologies involve (1) heating, (2) cooling, (3) mechanical treatment, (4) ultrasonication, and (5) evaporation. Lessons that can be learned from conventional food technologies are available from each of (1) through (4). Lesson(s) and understanding are additionally available from post-processing, i.e., extraction, as this is a further dispersive process. Cleaning commonly requires hot water, which increases energy, costs, and further environmental impact.
Extraction of food waste products can reduce and recover resources. Reported extraction technologies include ultrasound-assisted, microwave-assisted, enzyme-assisted, bioreactor-assisted, and/or high-pressure homogenizer technologies. Food waste generates some 113 Mt of CO 2 per annum 221 from resources used for biomass production, including water, fertilizer, pesticides, feed or seed, and energy. 222 An outcome from this recovery is bioactive compounds, 223 including healthpromoting additives and nutritional supplements, 224 or biofuels. Al-Dhabi et al. reported an ultrasound process that was claimed to be economically feasible and have a low energy demand for extraction of phytochemicals from exhausted coffee grounds. 225 Using ultrasound technology, Guandalini et al. demonstrated an improved pectin extraction of mango peel of 50% and, importantly, claimed that the pectin quality was maintained. 226 With microwave processing combined with deep eutectic solvents, 227 Pal and Jadeja conducted extraction of phenolic compounds from ripe mango. 228 Plazzotta et al. extracted valuable flavonoids and anthocyanins from frozen peach waste in <1 min via microwave technology. 229 Operating this technology with recycling, Escribàet al. 230 transformed vegetable oil and food fats into allyl esters 231 for use as ovicides against Cydia pononella L. 232 When strong oxidants, e.g., potassium dichromate, are used, cleaning effluent that forms a wastewater output impacts freshwater eutrophication potential (FEP).

Post-Processing
Operation. Cleaning, extraction, and decontamination remove deposits in heat exchangers, evaporators, and pipelines and increase water and chemical consumption. 233 Plasma, acknowledged as the fourth state of matter, is reportedly being used to decontaminate foods 9 via inactivation of microorganisms and can be used to remove biofilms, bacterial spores, fungi, and bacteria 234,235 with bacon, 236 cheese, 237 jam, 238 and squid 239 being reported applications. Plasma can also boost the flavor and aroma of foods. 240

CONCLUSIONS
Nanostructures provide a new and practical opportunity for food products via supramolecular architecture(s) to encapsulate bioactive molecules and to control targeted release.
Acceptance of these products in food processing is dependent on compliance with legislation and technological and economic sustainability. The economy of scale will also be important to ensure sustainability.
Only a limited number of nanofood processes have matured to industrial, or large pilot-scale, production. A sustainable methodology is therefore necessary to underpin developments in nanofood technology. It was found that this sustainable methodology must begin at the initial or laboratory scale.
Predictive sustainability assessment(s), including exploratory ex ante and anticipatory life cycle assessment(s), have been widely used to develop emerging technologies in chemistry and mining. To date, these have surprisingly not been used in food processing. It was hypothesized therefore that a methodology could be developed from sustainability assessments for conventional food technologies and applied practically to design for nanofood technology.
It was found that unit operations shared between conventional and emerging processes were a sufficiently pragmatic means for the development of sustainability. This is because there is a limited number of essential engineering operations including heating, drying, and post-processing, which determine the majority of conventional and nanofood technologies. Sustainability for these conventional processes is also well documented.
We conclude that this provides a quantitative means to incorporate sustainability during early process design for nanostructured foods. A major difficulty, however, to developing a generalized and quantitative methodology is that sustainability is unit operation-specific and food productspecific. Further development is therefore needed to create a transferable sustainability methodology.
However, the present findings will be of interest to food researchers and engineers, as well as manufacturers of process equipment.